CN105833986B - A forward and reverse flotation process for demanganese removal from manganese low-grade phosphate ore - Google Patents
A forward and reverse flotation process for demanganese removal from manganese low-grade phosphate ore Download PDFInfo
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- CN105833986B CN105833986B CN201610345277.7A CN201610345277A CN105833986B CN 105833986 B CN105833986 B CN 105833986B CN 201610345277 A CN201610345277 A CN 201610345277A CN 105833986 B CN105833986 B CN 105833986B
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- flotation
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- reverse flotation
- ore
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- 238000005188 flotation Methods 0.000 title claims abstract description 196
- 229910019142 PO4 Inorganic materials 0.000 title claims abstract description 52
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 title claims abstract description 52
- 239000010452 phosphate Substances 0.000 title claims abstract description 52
- 238000000034 method Methods 0.000 title claims abstract description 36
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 title claims description 63
- 239000011572 manganese Substances 0.000 title claims description 63
- 229910052748 manganese Inorganic materials 0.000 title claims description 63
- 239000003112 inhibitor Substances 0.000 claims abstract description 34
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims abstract description 31
- 239000002002 slurry Substances 0.000 claims abstract description 24
- 239000012141 concentrate Substances 0.000 claims abstract description 22
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical group [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims abstract description 18
- 239000000395 magnesium oxide Substances 0.000 claims abstract description 17
- 239000011574 phosphorus Substances 0.000 claims abstract description 17
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 17
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims abstract description 16
- 229910000029 sodium carbonate Inorganic materials 0.000 claims abstract description 8
- 239000003795 chemical substances by application Substances 0.000 claims description 58
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 40
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 24
- 239000000194 fatty acid Substances 0.000 claims description 24
- 229930195729 fatty acid Natural products 0.000 claims description 24
- -1 anionic fatty acid Chemical class 0.000 claims description 23
- 229920001353 Dextrin Polymers 0.000 claims description 17
- 239000004375 Dextrin Substances 0.000 claims description 17
- 235000019425 dextrin Nutrition 0.000 claims description 17
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Inorganic materials O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 claims description 17
- 239000002516 radical scavenger Substances 0.000 claims description 13
- 238000000227 grinding Methods 0.000 claims description 12
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 11
- 235000019353 potassium silicate Nutrition 0.000 claims description 11
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims description 11
- 229910001748 carbonate mineral Inorganic materials 0.000 claims description 8
- 229910052681 coesite Inorganic materials 0.000 claims description 8
- 229910052906 cristobalite Inorganic materials 0.000 claims description 8
- 239000000377 silicon dioxide Substances 0.000 claims description 8
- 229910052682 stishovite Inorganic materials 0.000 claims description 8
- 229910052905 tridymite Inorganic materials 0.000 claims description 8
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 5
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 3
- 238000002360 preparation method Methods 0.000 claims description 2
- 238000010979 pH adjustment Methods 0.000 claims 1
- 230000001629 suppression Effects 0.000 claims 1
- 239000000047 product Substances 0.000 abstract description 39
- 238000002156 mixing Methods 0.000 abstract description 22
- 239000006260 foam Substances 0.000 abstract description 7
- 239000002367 phosphate rock Substances 0.000 abstract description 2
- 238000004537 pulping Methods 0.000 abstract 2
- 238000003756 stirring Methods 0.000 abstract 2
- 229910004298 SiO 2 Inorganic materials 0.000 abstract 1
- 125000000129 anionic group Chemical group 0.000 abstract 1
- 239000012467 final product Substances 0.000 abstract 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 30
- 239000000344 soap Substances 0.000 description 15
- 239000011777 magnesium Substances 0.000 description 11
- 229910052500 inorganic mineral Inorganic materials 0.000 description 9
- 239000011707 mineral Substances 0.000 description 9
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 8
- 229910052749 magnesium Inorganic materials 0.000 description 8
- 229910001655 manganese mineral Inorganic materials 0.000 description 8
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 7
- 229910052710 silicon Inorganic materials 0.000 description 7
- 239000010703 silicon Substances 0.000 description 7
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 6
- 239000003814 drug Substances 0.000 description 6
- 238000004513 sizing Methods 0.000 description 6
- 238000001035 drying Methods 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000013065 commercial product Substances 0.000 description 3
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 3
- 229910052585 phosphate mineral Inorganic materials 0.000 description 3
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 230000000994 depressogenic effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000007667 floating Methods 0.000 description 2
- 238000005065 mining Methods 0.000 description 2
- MQMHJMFHCMWGNS-UHFFFAOYSA-N phosphanylidynemanganese Chemical compound [Mn]#P MQMHJMFHCMWGNS-UHFFFAOYSA-N 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 229910052604 silicate mineral Inorganic materials 0.000 description 2
- FWVCSXWHVOOTFJ-UHFFFAOYSA-N 1-(2-chloroethylsulfanyl)-2-[2-(2-chloroethylsulfanyl)ethoxy]ethane Chemical compound ClCCSCCOCCSCCCl FWVCSXWHVOOTFJ-UHFFFAOYSA-N 0.000 description 1
- KKCBUQHMOMHUOY-UHFFFAOYSA-N Na2O Inorganic materials [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- QLULGSLAHXLKSR-UHFFFAOYSA-N azane;phosphane Chemical compound N.P QLULGSLAHXLKSR-UHFFFAOYSA-N 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 229910052593 corundum Inorganic materials 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005456 ore beneficiation Methods 0.000 description 1
- 239000002686 phosphate fertilizer Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 229910001845 yogo sapphire Inorganic materials 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B9/00—General arrangement of separating plant, e.g. flow sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/001—Flotation agents
- B03D1/002—Inorganic compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/001—Flotation agents
- B03D1/004—Organic compounds
- B03D1/008—Organic compounds containing oxygen
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/001—Flotation agents
- B03D1/018—Mixtures of inorganic and organic compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D2201/00—Specified effects produced by the flotation agents
- B03D2201/007—Modifying reagents for adjusting pH or conductivity
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D2201/00—Specified effects produced by the flotation agents
- B03D2201/02—Collectors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D2201/00—Specified effects produced by the flotation agents
- B03D2201/06—Depressants
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D2203/00—Specified materials treated by the flotation agents; Specified applications
- B03D2203/02—Ores
- B03D2203/04—Non-sulfide ores
- B03D2203/06—Phosphate ores
Landscapes
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
本发明公开了一种锰质低品位磷矿脱锰正反浮选工艺，将锰镁质低品位磷矿石进行碎矿、磨矿之后，使锰矿物与磷矿物以及其他矿物单体解离，然后加入碳酸钠、正浮选抑制剂和正浮选捕收剂)进行搅拌调浆，矿浆进入正浮选工艺流程进行浮选，所得的槽内产品为正浮选尾矿；所获得的泡沫产品输送至反浮选工艺，调节PH值并加入反浮选抑制剂柠檬酸、反浮选脱锰阴离子型捕收剂进行搅拌调浆，调浆后所得矿浆进入反浮选工艺流程进一步进行反浮选，所得泡沫产品为反浮选尾矿，最终槽内产品为低MnO2、MgO、SiO2含量的磷精矿，经过浓缩、过滤、干燥得成品磷精矿，成功地实现锰质低品位磷矿选矿富集，提高了磷资源的利用率。
The invention discloses a forward and reverse flotation process for demanganese low-grade phosphate ore. Then add sodium carbonate, positive flotation inhibitor and positive flotation collector) for stirring and slurry mixing, the pulp enters the positive flotation process for flotation, and the obtained product in the tank is positive flotation tailings; the obtained The foam product is sent to the reverse flotation process, the pH value is adjusted, and the reverse flotation inhibitor citric acid and the reverse flotation demanganese anionic collector are added for stirring and pulping. After pulping, the obtained pulp enters the reverse flotation process for further processing. In reverse flotation, the foam product obtained is reverse flotation tailings, and the final product in the tank is phosphorus concentrate with low content of MnO 2 , MgO and SiO 2 . The beneficiation and enrichment of low-grade phosphate rock improves the utilization rate of phosphorus resources.
Description
Technical field
The invention belongs to ore dressing fields, and in particular to a kind of manganese matter low-grade phosphate ore demanganize direct reverse flotation technique.
Background technique
Phosphorus ore is the non-renewable basic material for producing phosphate fertilizer, phosphorus chemical product.But contain a large amount of manganese ores in phosphorus ore
Object includes psilomelane, pyrolusite and manganese spar etc., is preparing ammophos, manganese mineral can reduce quality and production energy rate, together
When influence phosphorus ammonium granulating and forming.Therefore must be by the content that certain process means reduce the manganese mineral in phosphorus concentrate
MnO2Content, and manganese matter low-grade phosphate ore is since various mineral inlay that relationship is complicated, disseminated grain size is thin, dissociative is poor, simultaneously
The high feature of the gangue minerals content such as silicate mineral, carbonate mineral and manganese mineral, development and utilization belong to worldwide difficulty
Topic.
Summary of the invention
It is positive and negative floating the purpose of the present invention is in view of the above shortcomings of the prior art, providing a kind of manganese matter low-grade phosphate ore demanganize
Technique is selected, the preparation process being related to is simple, separating effect is high, and the content that can effectively reduce gangue mineral (reduces MnO2、MgO、
SiO2Content), obtain the phosphorus concentrate of low manganese, low magnesium, low silicon, effectively overcome the application problem of the magnesia low-grade phosphate ore of manganese.
To achieve the above object, the technical solution adopted by the present invention are as follows:
A kind of manganese matter low-grade phosphate ore demanganize direct reverse flotation technique, it includes the following steps:
1) manganese matter low-grade phosphate ore is crushed, ore grinding；
2) direct flotation: addition pH regulator and waterglass, the pH value for controlling slurry is 9.5-11, be then added inhibitor and
Direct flotation collecting agent, inflation carry out direct flotation roughing, and gained froth pulp I further progress direct flotation is selected, selected (direct flotation
It is selected) gained tailing be chats, again add direct flotation collecting agent carry out direct flotation scan, with scan gained froth pulp II be
Chats merges with tailing obtained by selected (direct flotation is selected) returns to direct flotation roughing step, obtains froth pulp III, scans gained tail
Mine is as direct flotation tailing, and slurry temperature is 30-40 DEG C during entire direct flotation；
3) reverse flotation: adding sulfuric acid to above-mentioned select in froth pulp III of gained, and the pH value for adjusting ore pulp is 5-6, adds simultaneously
Adding citric acid and collecting agent in reverse floatation, inflation carry out the impurity such as the further demanganize of reverse flotation roughing, magnesium, reduce product in slot
MnO2、MgO、SiO2Content；Sulfuric acid progress reverse flotation is added into gained froth pulp IV to scan, product is anti-floating in scavenger flotation cell
Mine is chosen, returns and carries out reverse flotation roughing again, gained froth pulp V is reverse flotation tailing, and product is final essence in gained slot
Mine, the slurry temperature during entire reverse flotation are room temperature.
In above scheme, the chemical composition of the manganese matter low-grade phosphate ore: P2O5Grade is 9-11%, the mass content of MgO
For 1.5-2.5%, SiO2Mass content be 12-16%, MnO2Mass content be 1.0-3.5%.
In above scheme, the pH regulator is sodium carbonate.
In above scheme, the waterglass is 0.6-0.8kg/t with respect to the dosage of manganese matter low-grade phosphate ore.
In above scheme, the inhibitor is mixed by carbonate mineral inhibitor and dextrin, and wherein dextrin is relatively former
The dosage of mine (manganese matter low-grade phosphate ore) is 0.6-0.8kg/t, and hydrochlorate mineral inhibitor is with respect to raw ore (manganese matter low-grade phosphate ore)
Dosage be 0.6-0.8kg/t.
In above scheme, the carbonate mineral inhibitor is NO-2 (commercial product), and main component is the formaldehyde of naphthalene
Sulfonated bodies.
In above scheme, the direct flotation collecting agent is anionic fatty acid collecting agent TX-1 (commercial product).
In above scheme, the direct floatation process is that one roughing primary cleaning and once purging selection operation, chats return in proper order
It returns；Wherein roughing operation ore pulp emersion phosphate mineral in alkaline medium, discharge silicate gangue mineral reduce SiO2's
Content；Gained froth pulp into one without selected (not adding any medicament), this step be to froth pulp obtained by roughing into
One step flotation, obtains high-grade intermediate products；Using selected gained tailing as chats, direct flotation collecting agent is added again and is swept
Choosing, gained froth pulp are that chats merges return roughing operation with cleaner tailings, obtain froth pulp III, scan gained tailing and make
Be positive flotation tailing, and slurry temperature is 30-40 DEG C in entire floatation process.
In above scheme, in the direct flotation roughing step, dosage of the direct flotation collecting agent with respect to manganese matter low-grade phosphate ore
For 0.8-1.2kg/t；Direct flotation is scanned in step, and direct flotation collecting agent is 0.3- with respect to the dosage of manganese matter low-grade phosphate ore
0.5kg/t。
In above scheme, direct floatation process uses dextrin as the inhibitor of manganese mineral under alkaline condition, can reduce bubble
MnO in foam product2Content.
In above scheme, the reverse floatation process is one roughing and once purging selection operation, into gained froth pulp III
Sulfuric acid is added and adjusts its pH value to 5-6, reverse flotation inhibitor and collecting agent in reverse floatation (anionic fatty acid collecting is then added
Agent) it sizes mixing again, inflation carries out reverse flotation roughing, reduces the MnO of product in slot2, content of MgO, then proceed to be added sulfuric acid into
Row reverse flotation is scanned, and product is reverse flotation chats in scavenger flotation cell, is returned reverse flotation roughing (de-magging, demanganize), gained in scavenger flotation cell
Froth pulp is reverse flotation tailing, and last products obtained therefrom is final concentrate in initial separatory cell, the ore pulp temperature during entire reverse flotation
Degree is room temperature condition；Direct flotation tailing, reverse flotation tailing merge discharge and stack.
In above scheme, the reverse flotation inhibitor is citric acid, and the dosage of opposite manganese matter low-grade phosphate ore is 0.6-
0.9kg/t。
In above scheme, the collecting agent in reverse floatation is anionic fatty acid collecting agent TXO-2 (commercial product),
The dosage of opposite manganese matter low-grade phosphate ore is 0.3-0.5kg/t.
In above scheme, during reverse flotation is scanned, sulfuric acid phase is 1-3kg/t to the ratio of manganese matter low-grade phosphate ore.
In above scheme, the technique of the manganese matter low-grade phosphate ore demanganize uses direct reverse flotation technique, carries out first just
Flotation inhibits gangue mine as combined depressant, that is, waterglass, NO-2 joint dextrin using three kinds of inhibitor in alkaline medium
Object, emersion phosphate mineral reduce the content of gangue mineral；Then reverse flotation is carried out, in the condition that slurry pH is 5.2-5.5
Under, using the collecting agent flotation manganese mineral with enrichment manganese mineral, reduce the manganese content of phosphorus concentrate.
In above scheme, reverse floatation process under mildly acidic conditions, using sulfuric acid and citric acid respectively as pH regulator
And inhibitor, the fatty acid anion type surfactant of joint enrichment manganese ore carry out flotation as collecting agent, further decrease
MnO in phosphorus concentrate product2Content.
The present invention is principle are as follows: the present invention uses the positive and negative floatation process of manganese matter low-grade phosphate ore, first in alkaline medium
Inhibit gangue mineral, emersion phosphate mineral, drop as combined depressant (waterglass, NO-2 and dextrin) using three kinds of inhibitor
The content of low gangue mineral；Then reverse flotation is carried out in weak acidic medium, and manganese mineral is enriched with using sulfuric acid and combined citric acid
Anion collecting agent be further backing out carbonate and gangue mineral containing manganese, reduce MnO2、MgO、SiO2Content, using this
Technique can obtain the phosphorus concentrate of the low Mg low-Si of low manganese.
Compared with prior art, the invention has the benefit that the present invention can effectively reduce manganese using direct reverse flotation technique
The content of silicate mineral, carbonate mineral and manganese mineral in matter low-grade phosphate ore obtains the phosphorus essence of low magnesium, low manganese, low silicon
Mine successfully realizes manganese matter low-grade phosphate ore beneficiation enrichment, improves the utilization rate of phosphor resource, overcoming existing floatation process cannot
It is efficiently applied to the technical problem of manganese matter low-grade phosphate ore ore dressing.
Detailed description of the invention
Fig. 1 is the flow chart of manganese matter low-grade phosphate ore demanganize direct reverse flotation technique described in embodiment 1.
Specific embodiment
For a better understanding of the present invention, below with reference to the embodiment content that the present invention is furture elucidated, but the present invention is not
It is limited only to the following examples.
Unless specific instructions, the reagent used is commercially available chemical reagent or industrial products to following embodiment.
In embodiment 3~5, the manganese matter low-grade phosphate ore stone of use is formed from its primary chemical of Hubei Huang Mailing are as follows: P2O5
Grade is 9-11%, and the mass content of MgO is 1.5-2.5%, SiO2Mass content be 12-16%, MnO2Content 1.5-
3.5%.
In following embodiment, the carbonate mineral inhibitor used is NO-2, by the limited public affairs of Xiaogan City Tianxiang mining industry science and technology
Company, department provides；The direct flotation collecting agent used is anionic fatty acid collecting agent TX-1, by Xiaogan City Tianxiang mining industry section
Skill Co., Ltd provides；The collecting agent in reverse floatation used is anionic fatty acid collecting agent TXO-2, by Xiaogan City Tianxiang mine
Industry Science and Technology Ltd. provides.
Embodiment 1
A kind of manganese matter low-grade phosphate ore demanganize direct reverse flotation technique, flow chart is shown in Fig. 1, wherein the manganese matter used is low-grade
Rock phosphate in powder is Hubei manganese matter low-grade phosphate ore, primary chemical composition are as follows:
| Element species | P2O5 | MgO | Fe2O3 | Al2O3 | CaO | SiO2 | Na2O | K2O | MnO2 | CO2 | F | TiO2 |
| Content/% | 10.62 | 1.96 | 2.37 | 3.18 | 4.68 | 14.78 | 30.28 | 0.40 | 3.05 | 31.53 | 0.07 | 0.34 |
Specific step is as follows:
It carries out manganese matter low-grade phosphate ore (raw ore) to be crushed to -2mm, ore grinding is then carried out using ore mill, until ore grinding is thin
Degree be -0.074mm ore particle mass fraction account for 68.6% or so, then plus water size mixing into ore pulp solid concentration be 340g/L,
Then it flows into agitator, sodium carbonate (dosage of opposite raw ore is 3kg/t) and waterglass (opposite raw ore is added into ore pulp
Dosage is 0.7kg/t) adjustment ore pulp pH value be 9.5, then be added inhibitor (it is mixed by Carbonate inhibitor NO-2 with dextrin
Close, NO-2 is 0.8kg/t with respect to the ratio of raw ore, and dextrin is 0.8kg/t with respect to the ratio of raw ore) and direct flotation collecting agent
(anionic fatty acid (soap) class collecting agent TX-1, dosage are 0.9kg/t with respect to the ratio of raw ore) sizes mixing, slurry temperature
It is 35 DEG C, direct flotation roughing operation is entered after sizing mixing and is inflated flotation, obtains direct flotation roughing froth pulp I and carry out direct flotation
Selected, any medicament is not added in selected operation, obtains high-grade selected froth pulp；Using selected gained tailing as chats, after
(anionic fatty acid (soap) class collecting agent TX-1, dosage are 0.4kg/ with respect to the ratio of raw ore to continuous addition direct flotation collecting agent
T) it is scanned, scanning gained froth pulp II is that chats merges return roughing operation with cleaner tailings, froth pulp III is obtained,
Tailing is scanned as direct flotation tailing, slurry temperature is 35 DEG C during entire direct flotation；
Gained froth pulp III is flowed into reverse flotation stirred tank, sulfuric acid is added thereto and adjusts its pH value to 5.5, then
Reverse flotation inhibitor (citric acid, the dosage of opposite raw ore are 0.6kg/t) and collecting agent in reverse floatation (anionic fatty acid is added
(soap) class collecting agent TXO-2, the dosage of opposite raw ore are 0.3kg/t) it sizes mixing again, reverse flotation roughing is carried out, reduces in slot and produces
The MnO of product2, content of MgO, sulfuric acid is then continuously added into gained froth pulp IV (dosage of opposite raw ore is 2.0kg/t)
It carries out reverse flotation to scan, product is reverse flotation chats in scavenger flotation cell, is returned reverse flotation roughing (de-magging, demanganize), institute in scavenger flotation cell
Froth pulp V is reverse flotation tailing, last products obtained therefrom is final concentrate in initial separatory cell, and last concentrated, filtering, drying are
Obtain the phosphorus concentrate finished product of low magnesium, low silicon, low manganese；Slurry temperature during entire reverse flotation is room temperature condition, direct flotation tailing,
Reverse flotation tailing merges discharge and stacks.
In the phosphorus concentrate finished product of the low manganese of the low Mg low-Si of the present embodiment gained, P2O5Grade be 38.59%, the rate of recovery is
91.51%, MnO in concentrate2Content 0.61%, the content 0.28% of MgO；Reverse flotation tailing P2O5Grade 8.18%, direct flotation
Tailing P2O5Grade is down to 0.87%.
Embodiment 2
A kind of manganese matter low-grade phosphate ore floatation process, the specific steps are as follows:
It carries out manganese matter low-grade phosphate ore (raw ore is formed with embodiment 1) to be crushed to -2mm, then be carried out using ore mill
Ore grinding, until the ore particle mass fraction that grinding fineness is -0.074mm accounts for 68% or so, then plus water solid of sizing mixing into ore pulp is dense
Degree is 340g/L, is then flowed into agitator, and sodium carbonate (dosage of opposite raw ore is 3.5kg/t) and water glass are added into ore pulp
The pH value of glass (dosage of opposite raw ore is 0.8kg/t) adjustment ore pulp is 10.0, and inhibitor is then added, and (it is inhibited by carbonate
Agent NO-2 is mixed with dextrin, and NO-2 is 0.8kg/t with respect to the ratio of raw ore, and dextrin is 0.8kg/t with respect to the ratio of raw ore)
With direct flotation collecting agent (anionic fatty acid (soap) class collecting agent TX-1, dosage with respect to raw ore ratio be 0.7kg/t) into
Row is sized mixing, and slurry temperature is 35 DEG C, and direct flotation roughing operation is entered after sizing mixing and is inflated flotation, obtains direct flotation roughing foam
Product I progress is selected, and any medicament is not added in selected operation, obtains high-grade selected froth pulp；With selected gained tailing
For chats, direct flotation collecting agent (anionic fatty acid (soap) class collecting agent TX-1, ratio of the dosage with respect to raw ore are continuously added
It is scanned for 0.5kg/t), scanning gained froth pulp II is that chats merges return roughing operation with cleaner tailings, obtains foam
Product I II scans tailing as direct flotation tailing, and slurry temperature is 35 DEG C during entire direct flotation；
Gained froth pulp III is flowed into reverse flotation stirred tank, sulfuric acid is added thereto and adjusts its pH value to 5.0, then
Reverse flotation inhibitor (citric acid, the dosage of opposite raw ore are 0.6kg/t) and collecting agent in reverse floatation (anionic fatty acid is added
(soap) class collecting agent TXO-2, the dosage of opposite raw ore are 0.45kg/t) it sizes mixing again, reverse flotation roughing is carried out, reduces in slot and produces
The MnO of product2, content of MgO, sulfuric acid is then continuously added into gained froth pulp IV (dosage of opposite raw ore is 2.0kg/t)
It carries out reverse flotation to scan, product is reverse flotation chats in scavenger flotation cell, is returned reverse flotation roughing (de-magging, demanganize), institute in scavenger flotation cell
Froth pulp V is reverse flotation tailing, last products obtained therefrom is final concentrate in initial separatory cell, and last concentrated, filtering, drying are
Obtain the phosphorus concentrate finished product of low magnesium, low silicon, low manganese；Slurry temperature during entire reverse flotation is room temperature condition, direct flotation tailing,
Reverse flotation tailing merges discharge and stacks.
In the phosphorus concentrate finished product of the low manganese of the low Mg low-Si of the present embodiment gained, P2O5Grade be 38.68%, the rate of recovery is
90.11%, MnO in concentrate2Content 0.65%, the content 0.18% of MgO；Reverse flotation tailing P2O5Grade 9.61%, direct flotation
Tailing P2O5Grade is down to 0.93%.
Embodiment 3
A kind of manganese matter low-grade phosphate ore floatation process, the specific steps are as follows:
It carries out manganese matter low-grade phosphate ore (raw ore) to be crushed to -2mm, ore grinding is then carried out using ore mill, until ore grinding is thin
Degree is that the ore particle mass fraction of -0.074mm accounts for 68% or so, and then plus water sizes mixing into ore pulp solid concentration for 340g/L, so
It flows into agitator afterwards, sodium carbonate (dosage of opposite raw ore is 4kg/t) and the waterglass (use of opposite raw ore is added into ore pulp
Amount be 0.7kg/t) adjustment ore pulp pH value be 10.5, then addition inhibitor (it is mixed by Carbonate inhibitor NO-2 with dextrin
Close, NO-2 is 0.6kg/t with respect to the ratio of raw ore, and dextrin is 0.6kg/t with respect to the ratio of raw ore) and direct flotation collecting agent
(anionic fatty acid (soap) class collecting agent TX-1, dosage are 0.8kg/t with respect to the ratio of raw ore) sizes mixing, slurry temperature
It is 35 DEG C, direct flotation roughing operation is entered after sizing mixing and is inflated flotation, acquisition direct flotation roughing froth pulp I progress is selected,
Any medicament is not added in selected operation, obtains high-grade selected froth pulp；Using selected gained tailing as chats, continuously add
Direct flotation collecting agent (anionic fatty acid (soap) class collecting agent TX-1, dosage are 0.5kg/t with respect to the ratio of raw ore) carries out
It scans, scanning gained froth pulp II is that chats merges return roughing operation with cleaner tailings, obtains froth pulp III, scans tail
Mine is as direct flotation tailing, and slurry temperature is 35 DEG C during entire direct flotation；
Gained froth pulp III flows into reverse flotation stirred tank, and sulfuric acid is added thereto and adjusts its pH value to 6, is then added
Reverse flotation inhibitor (citric acid, the dosage of opposite raw ore are 0.3kg/t) and collecting agent in reverse floatation (anionic fatty acid (soap)
Class collecting agent TXO-2, the dosage of opposite raw ore are 0.3kg/t) it sizes mixing again, reverse flotation roughing is carried out, product in slot is reduced
MnO2, content of MgO, sulfuric acid (dosage of opposite raw ore is 1.0kg/t) is then continuously added into gained froth pulp IV and is carried out
Reverse flotation is scanned, and product is reverse flotation chats in scavenger flotation cell, is returned reverse flotation roughing (de-magging, demanganize), gained bubble in scavenger flotation cell
Foam product V is reverse flotation tailing, and last products obtained therefrom is final concentrate in initial separatory cell, it is last it is concentrated, filter, be drying to obtain it is low
Magnesium, low silicon, low manganese phosphorus concentrate finished product；Slurry temperature during entire reverse flotation is room temperature condition, and direct flotation tailing instead floats
It selects tailing to merge discharge to stack.
Embodiment 4
A kind of manganese matter low-grade phosphate ore floatation process, the specific steps are as follows:
It carries out manganese matter low-grade phosphate ore (raw ore) to be crushed to -2mm, ore grinding is then carried out using ore mill, until ore grinding is thin
Degree is that the ore particle mass fraction of -0.074mm accounts for 68% or so, and then plus water sizes mixing into ore pulp solid concentration for 340g/L, so
It flows into agitator afterwards, sodium carbonate (dosage of opposite raw ore is 3.5kg/t) and waterglass (opposite raw ore is added into ore pulp
Dosage is 0.6kg/t) adjustment ore pulp pH value be 10, then be added inhibitor (it is mixed by Carbonate inhibitor NO-2 with dextrin
Close, NO-2 is 0.8kg/t with respect to the ratio of raw ore, and dextrin is 0.8kg/t with respect to the ratio of raw ore) and direct flotation collecting agent
(anionic fatty acid (soap) class collecting agent TX-1, dosage are 0.8kg/t with respect to the ratio of raw ore) sizes mixing, slurry temperature
It is 35 DEG C, direct flotation roughing operation is entered after sizing mixing and is inflated flotation, acquisition direct flotation roughing froth pulp I progress is selected,
Any medicament is not added in selected operation, obtains high-grade selected froth pulp；Using selected gained tailing as chats, continuously add
Direct flotation collecting agent (anionic fatty acid (soap) class collecting agent TX-1, dosage are 0.4kg/t with respect to the ratio of raw ore) carries out
It scans, scanning gained froth pulp II is that chats merges return roughing operation with cleaner tailings, obtains froth pulp III, scans tail
Mine is as direct flotation tailing, and slurry temperature is 35 DEG C during entire direct flotation；
Gained froth pulp III flows into reverse flotation stirred tank, and sulfuric acid is added thereto and adjusts its pH value to 5.8, then plus
Enter reverse flotation inhibitor (citric acid, the dosage of opposite raw ore are 0.6kg/t) and anionic fatty-acid collector (anionic
Fatty acid (soap) class collecting agent TXO-2, the dosage of opposite raw ore are 0.3kg/t) it sizes mixing again, reverse flotation roughing is carried out, is reduced
The MnO of product in slot2, content of MgO, sulfuric acid is then continuously added into gained froth pulp IV, and (dosage of opposite raw ore is
It 2.0kg/t) carries out reverse flotation to scan, product is reverse flotation chats in scavenger flotation cell, returns reverse flotation roughing (de-magging, demanganize), sweeps
Selecting gained froth pulp V in slot is reverse flotation tailing, and last products obtained therefrom is final concentrate in initial separatory cell, last concentrated, mistake
Filter, be drying to obtain the phosphorus concentrate finished product of low magnesium, low silicon, low manganese；Slurry temperature during entire reverse flotation is room temperature condition, just
Flotation tailing, reverse flotation tailing merge discharge and stack.
Embodiment 5
A kind of manganese matter low-grade phosphate ore floatation process, the specific steps are as follows:
It carries out manganese matter low-grade phosphate ore (raw ore) to be crushed to -2mm, ore grinding is then carried out using ore mill, until ore grinding is thin
Degree is that the ore particle mass fraction of -0.074mm accounts for 68% or so, and then plus for 34g/L, then water sizes mixing into ore pulp solid concentration
It flows into agitator, sodium carbonate (dosage of opposite raw ore is 5kg/t) and the waterglass (dosage of opposite raw ore is added into ore pulp
The pH value that ore pulp is adjusted for 0.6kg/t) be 11, then addition inhibitor (it mixed with dextrin by Carbonate inhibitor NO-2 and
At NO-2 is 0.7kg/t with respect to the ratio of raw ore, and dextrin is 0.7kg/t with respect to the ratio of raw ore) and direct flotation collecting agent (yin
Ionic fatty acid (soap) class collecting agent TX-1, dosage are 1kg/t with respect to the ratio of raw ore) it sizes mixing, slurry temperature 35
DEG C, direct flotation roughing operation is entered after sizing mixing and is inflated flotation, acquisition direct flotation roughing froth pulp I progress is selected, selected
Any medicament is not added in operation, obtains high-grade selected froth pulp；Using selected gained tailing as chats, continuously adds and top-up
Collecting agent (anionic fatty acid (soap) class collecting agent TX-1, dosage are 0.3kg/t with respect to the ratio of raw ore) is selected to be scanned,
Scanning gained froth pulp II is that chats merges return roughing operation with cleaner tailings, obtains froth pulp III, scans tailing conduct
Direct flotation tailing, slurry temperature is 35 DEG C during entire direct flotation；
Gained froth pulp III flows into reverse flotation stirred tank, and sulfuric acid is added thereto and adjusts its pH value to 5, is then added
Reverse flotation inhibitor (citric acid, the dosage of opposite raw ore are 0.4kg/t) and collecting agent in reverse floatation (anionic fatty acid (soap)
Class collecting agent TXO-2, the dosage of opposite raw ore are 0.4kg/t) it sizes mixing again, reverse flotation roughing is carried out, product in slot is reduced
MnO2, content of MgO, sulfuric acid (dosage of opposite raw ore is 1.5kg/t) is then continuously added into gained froth pulp IV and is carried out
Reverse flotation is scanned, and product is reverse flotation chats in scavenger flotation cell, is returned reverse flotation roughing (de-magging, demanganize), gained bubble in scavenger flotation cell
Foam product V is reverse flotation tailing, and last products obtained therefrom is final concentrate in initial separatory cell, it is last it is concentrated, filter, be drying to obtain it is low
Magnesium, low silicon, low manganese phosphorus concentrate finished product；Slurry temperature during entire reverse flotation is room temperature condition, and direct flotation tailing instead floats
It selects tailing to merge discharge to stack.
The foregoing is merely the preferred embodiment of the present invention, it is noted that comes for those of ordinary skill in the art
It says, without departing from the concept of the premise of the invention, make several modifications and variations, these belong to protection model of the invention
It encloses.
Claims (7)
1. a kind of manganese matter low-grade phosphate ore demanganize direct reverse flotation technique, it includes the following steps:
1) manganese matter low-grade phosphate ore is crushed, ore grinding；
2) direct flotation: addition pH regulator and waterglass, the pH value for controlling slurry is 9.5-11, and inhibitor is then added and top-ups
Collecting agent is selected, inflation carries out direct flotation roughing, and gained froth pulp I further progress direct flotation is selected, and selected gained tailing is
Chats adds direct flotation collecting agent in direct flotation rougher tailings and carries out direct flotation and scan, again to scan gained froth pulp II
Merge for chats with selected gained tailing and return to direct flotation roughing step, obtains froth pulp III through direct flotation is selected, scan gained
Tailing is as direct flotation tailing, and slurry temperature is 30-40 DEG C during entire direct flotation；
3) reverse flotation: adding sulfuric acid into gained froth pulp III, and the pH value for adjusting ore pulp is 5-6, while adding reverse flotation suppression
Preparation and collecting agent in reverse floatation, inflation carry out reverse flotation roughing, and sulfuric acid progress reverse flotation is added into gained froth pulp IV and sweeps
Choosing returns using product in scavenger flotation cell as reverse flotation chats and carries out reverse flotation roughing again, and reverse flotation scans gained froth pulp V
For reverse flotation tailing, product is final concentrate in slot obtained by reverse flotation roughing, and the slurry temperature during entire reverse flotation is room
Warm condition；
The inhibitor is mixed by carbonate mineral inhibitor and dextrin；The carbonate mineral inhibitor is NO-2,
Main component is the formaldehyde sulfonated bodies of naphthalene；
The chemical composition of the manganese matter low-grade phosphate ore: P2O5Grade is 9-11%, and the mass content of MgO is 1.5-2.5%, SiO2
Mass content be 12-16%, MnO2Mass content be 1.0-3.5%；
The collecting agent in reverse floatation is anionic fatty acid collecting agent TXO-2, the dosage of opposite manganese matter low-grade phosphate ore
For 0.3-0.5kg/t.
2. manganese matter low-grade phosphate ore demanganize direct reverse flotation technique according to claim 1, which is characterized in that the pH adjustment
Agent is sodium carbonate.
3. manganese matter low-grade phosphate ore demanganize direct reverse flotation technique according to claim 1, which is characterized in that the waterglass
The dosage of opposite manganese matter low-grade phosphate ore is 0.6-0.8kg/t.
4. manganese matter low-grade phosphate ore demanganize direct reverse flotation technique according to claim 1, which is characterized in that the dextrin phase
Dosage to manganese matter low-grade phosphate ore is 0.6-0.8kg/t, dosage of the carbonate mineral inhibitor with respect to manganese matter low-grade phosphate ore
For 0.6-0.8kg/t.
5. manganese matter low-grade phosphate ore demanganize direct reverse flotation technique according to claim 1, which is characterized in that the direct flotation
Collecting agent is anionic fatty acid collecting agent TX-1；In direct flotation roughing step, direct flotation collecting agent product low with respect to manganese matter
The dosage of position phosphorus ore is 0.8-1.2kg/t；Direct flotation is scanned in step, use of the direct flotation collecting agent with respect to manganese matter low-grade phosphate ore
Amount is 0.3-0.5kg/t.
6. manganese matter low-grade phosphate ore demanganize direct reverse flotation technique according to claim 1, which is characterized in that the reverse flotation
Inhibitor is citric acid, and the dosage of opposite manganese matter low-grade phosphate ore is 0.6-0.9kg/t.
7. manganese matter low-grade phosphate ore demanganize direct reverse flotation technique according to claim 1, which is characterized in that reverse flotation is scanned
In the process, sulfuric acid phase is 1-3kg/t to the dosage of manganese matter low-grade phosphate ore.
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| CN108751150A (en) * | 2018-08-22 | 2018-11-06 | 贵州大学 | A method of being enriched with low-grade phosphate ore stone using low molecular weight organic acid |
| CN108993779A (en) * | 2018-09-10 | 2018-12-14 | 湖北省黄麦岭磷化工有限责任公司 | Manganese phosphorus direct reverse flotation technique drops in low-grade manganese matter phosphorite mine demagging |
| CN109225649B (en) * | 2018-10-29 | 2020-06-30 | 贵州川恒化工股份有限公司 | Phosphorite layer a ore reverse flotation composite collecting agent and preparation method thereof |
| CN110142145A (en) * | 2019-06-04 | 2019-08-20 | 瓮福（集团）有限责任公司 | The technique of sesquichloride and magnesium addition in a kind of flotation removing silicon calcium collophanite |
| CN110455781B (en) * | 2019-08-26 | 2022-03-25 | 北矿检测技术有限公司 | LIBS (laser induced breakdown Spectroscopy) online detection system for phosphate ore dressing system and application of LIBS online detection system |
| CN111940147A (en) * | 2019-12-10 | 2020-11-17 | 湖北大峪口化工有限责任公司 | Application of naphthalene-based superplasticizer as collophanite beneficiation inhibitor |
| CN112588445B (en) * | 2020-10-09 | 2022-09-20 | 太原钢铁(集团)有限公司 | Operating method for stabilizing reverse flotation production |
| CN113908994B (en) * | 2021-09-27 | 2023-11-21 | 南华大学 | Flotation method of low-grade phosphorite |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5542545A (en) * | 1994-04-12 | 1996-08-06 | Ying Xue Yu | Process for phosphate beneficiation |
| CN1730161A (en) * | 2005-07-30 | 2006-02-08 | 中蓝连海设计研究院 | Collophanite direct flotation and reverse flotation technique |
| CN103480483A (en) * | 2013-10-11 | 2014-01-01 | 武汉工程大学 | Phosphate dense medium mineral separation and direct-reverse floatation combined technology |
| CN104801427A (en) * | 2015-05-11 | 2015-07-29 | 中蓝连海设计研究院 | Direct and reverse flotation technique for high-magnesium low-grade phosphorus ore coarse grains |
| CN104907183A (en) * | 2015-07-03 | 2015-09-16 | 武汉工程大学 | Silica-calcia low-grade collophanite positive and inverse floatation process |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101716556B (en) * | 2010-01-11 | 2013-04-24 | 花垣县强桦矿业有限责任公司 | Floating and enriching method of low-grade manganese dioxide ore |
| CN101733194B (en) * | 2010-01-21 | 2012-10-03 | 中南大学 | Ore dressing method of low-grade manganese carbonate ore |
| CN102671771B (en) * | 2012-05-02 | 2013-09-11 | 广西大学 | Method for floating and separating zinc silicate and kutnahorite |
| CN102861674B (en) * | 2012-09-29 | 2014-11-19 | 北京科技大学 | A kind of flotation method of soft manganese ore |
| BR112015018615B1 (en) * | 2013-02-05 | 2019-03-12 | Vale S/A | PROCESS TO CONCENTRATE MANGANESE FROM THE WASTE OF A BENEFITING PLAN CONTAINING A LOW MANGANESE MINERAL |
| CN103212484B (en) * | 2013-04-18 | 2015-05-20 | 武汉工程大学 | Phosphorite reverse flotation process |
| CN105413853B (en) * | 2015-12-10 | 2017-09-01 | 中国地质科学院郑州矿产综合利用研究所 | Enrichment method of manganese boracite |
-
2016
- 2016-05-23 CN CN201610345277.7A patent/CN105833986B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5542545A (en) * | 1994-04-12 | 1996-08-06 | Ying Xue Yu | Process for phosphate beneficiation |
| CN1730161A (en) * | 2005-07-30 | 2006-02-08 | 中蓝连海设计研究院 | Collophanite direct flotation and reverse flotation technique |
| CN103480483A (en) * | 2013-10-11 | 2014-01-01 | 武汉工程大学 | Phosphate dense medium mineral separation and direct-reverse floatation combined technology |
| CN104801427A (en) * | 2015-05-11 | 2015-07-29 | 中蓝连海设计研究院 | Direct and reverse flotation technique for high-magnesium low-grade phosphorus ore coarse grains |
| CN104907183A (en) * | 2015-07-03 | 2015-09-16 | 武汉工程大学 | Silica-calcia low-grade collophanite positive and inverse floatation process |
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